WO1999023046A1

WO1999023046A1 - Slag for cementing a well, in particular an oil well

Info

Publication number: WO1999023046A1
Application number: PCT/FR1998/002339
Authority: WO
Inventors: Christine Noik; Alain Rivereau; Christian Vernet
Original assignee: Bouygues; Institut Francais Du Petrole
Priority date: 1997-11-03
Filing date: 1998-11-02
Publication date: 1999-05-14
Also published as: NO993132D0; EP0950034B1; US6332920B1; DK0950034T3; NO993132L; NO325917B1; FR2770517A1; CA2276714A1; DE69804198T2; EP0950034A1; CA2276714C; FR2770517B1; DE69804198D1

Abstract

The invention concerns oil well cementation, using a slag comprising a hydraulic binder, a microsilica, a mineral additive, a superplasticizer and water, in predetermined conditions of blending and percentage. The figure represents three compositions of the invention but which differ concerning the origin of the microsilica. The invention is useful in particular for cementing an oil well.

Description

WELL CEMENTING A WELL, ESPECIALLY A WELL

OILER

DESCRIPTION

Technical area

The present invention relates to a slag for cementing a well, in particular a well for exploring or exploiting underground deposits, such as hydrocarbon or geothermal deposits.

Well cementing is a very specific operation requiring the injection of a cement slag through tubes (casing or tubing) by pumping from the surface. One of the primary purposes of these operations is to cement the annular space between the outside of the casing tube and the drilled hole. Other cementing operations, well known to those skilled in the art, may also be concerned, for example the installation of plugs or “squeeze” operations. The well, interior space and annular space, is filled with a fluid, generally the drilling fluid of the previous drilling phase, or with a fluid of similar composition. The cement slag must be placed in the annular space by circulation while expelling the original annular fluid to the surface. The main functions of petroleum cement slag are in particular to seal the annular space to the fluids contained in rocks, gas, oil or water and to mechanically hold the tubes in the drilled hole. For this, the compressive strength characteristic is essential. Taking into account the installation of the slag by circulation, the rheology control is also very important, as well as the possibility of using additives adapted to particular conditions, for example filtrate reducers, retarders or setting accelerators , dispersing agents, defoamers, lightening or weighting agents.

State of the art

Current formulations of a cement slag for cementing oil wells include an amount of water of the order of 45% of the weight of the cement, which considerably limits the mechanical properties of hardened slag, in particular its resistance to compression.

On the other hand, cement formulations are known which lead to very superior mechanical properties, as described for example in European patent EP 0 518 777, but which are not suitable as well cementing slag, if only due to their insufficient proportion of water.

Statement of the invention

The problem therefore arises of defining an optimized slag composition, the rheology of which is suitable for cementing an oil well or the like, which comprises a quantity of water significantly lower than that of the slag hitherto recommended for this application, and which, after hardening, has mechanical characteristics far superior to those of the cementing slag of the prior art. These results are obtained, according to the invention, with a slag which comprises: - a hydraulic binder from the group consisting of Portland cements class G (API), Portland cements class H (API) and other hydraulic binders with a low aluminate content, - a microsilica with a particle size in the range 0.1 to 0 , 50 micrometers, at a rate of 20 to 35% by weight relative to the hydraulic binder.

- an addition of medium, inorganic and / or organic particles, of particle size included in the range 0.5-200 micrometers, at a rate of; 20 to 35% by weight relative to the hydraulic binder, the amount of said addition of medium particles being less than or equal to the amount of microsilica,

a water-soluble superplasticizer and / or fluidizer in a proportion of between 1% and 3% by weight relative to the hydraulic binder, and

- water in an amount at most equal to 30% of the weight of the hydraulic binder.

Preferably, for a given composition, the amount of water is slightly greater than that just sufficient to fill the voids between the grains of the composition, so as to ensure the essential rheology.

In preferred embodiments, the slag composition of the invention still has one or more of the following characteristics:

- The hydraulic binder is a Portland cement, class G.

- The ^hydraulic binder is composed of particles whose sizes are distributed in the range 0.1-100 micrometers.

- The hydraulic binder consists of particles whose sizes are distributed in the range 10 to 50 micrometers.

- Microsilica is a silica fume from the zirconium industry. - The microsilica is present at a rate of 20-30% by weight relative to the hydraulic binder.

- The microsilica is present at a rate of 20 to 25% by weight relative to the hydraulic binder. - The microsilica is made up of agglomerates of particles whose average size is close to 3 micrometers.

- The addition of medium particles is an organic addition of plastic balls, for example of polystyrene. - ₇

- The addition of medium particles is a mineral addition chosen from silica, clay, glass beads, metal salts, baryte, hematite and ilmenite. - The addition of medium particles is a mineral addition of siliceous particles.

- The addition of medium particles is present at a rate of 20 to 30% by weight relative to the hydraulic binder.

- The addition of medium particles is a mineral addition of silica sand whose particles have sizes distributed in the range 5-200 micrometers.

- The addition of medium particles is a mineral addition of silica sand whose particles have an average size close to 50 micrometers. - The addition of medium particles is a mineral addition of ground quartz.

- The water-soluble agent is composed of a highly ionized polymer or copolymer derived from sulfonated functions and / or from phosphate, phosphonate, carboxylate.

- The water-soluble agent is an agent from the group consisting of naphthalene sulfonate, lignosulfate, melanin and the like.

- The water-soluble agent is a fluidizer containing sulfonated or phosphated functions.

- The amount of water is preferably included in the / 23046

range 20-30% of the weight of the hydraulic binder.

Brief description of the drawings

Examples of embodiments of the invention and comparative tests will be described below, with reference to the figures in the accompanying drawing.

- Figure 1 shows the stress curves τ shear γ at 80 ° C of three slag formulations which differ in the microsilica used;

- Figure 2 shows the stress curves τ - shear γ at 80 ° C for two slag formulations which differ in the nature of the fluidizer used;

- Figure 3 shows the τ shear stress curves γ at 20 ° C for five slag formulations of different particle sizes, and Figure 4 shows the τ shear γ stress curves at 20 ° C for two slag formulations differing in particular in their water content.

Detailed description of the embodiments

In the following examples, a Portland cement was used corresponding to petroleum standards Class G. The cement powder, of a very wide particle size range (between 0.1 and 100 μm) having a D50 value of approximately 14 μm and a BET specific surface of approximately 1 m / g, has grains of very varied angular shapes.

The D50 value represents the particle size below which 50% of the particles have a dimension smaller than this D50 value. Silica, used as a mineral addition of medium particles, is in the form of ground quartz and is mainly composed of silicon oxide, traces of aluminum, iron and potassium. The very angular grains have a granular range of between 0.5 and 200 μm, preferably between 1 and 150 μm, a D50 value of approximately 42 μm, and a specific surface area measured by BET of 0.46 m / g .

The microsilica used (microsilica a) is of structure is of amorphous structure, the size of the agglomerates constituting the powder varies from 1 to 50 μm. Observation with a scanning electron microscope shows that the powder grains are made up of associations of spherical elementary particles (0.1 to 2 μm). These particles are amorphous microspheres with a density close to 2.2. The D50 value is 3 μm.

Finally, the superplasticizer is the fluidizer D80 (Dowell) which is a sodium polynaphthalene sulfonate containing 40% by mass of dry matter and 60% of water.

This polymer makes it possible to fluidize the mixture and to reduce the amount of water used for the same viscosity. It also acts as a retarder.

Thus, the D50 values of the cement, of the average particles of the silica type and of the microsilica are respectively 14, 42 and 3 μm. It is clear that the three granular products used (cement, addition and microsilica) have particle sizes which are relatively distributed among themselves in a specific manner taking into account the value of their D50. We will not depart from the invention if we use other particles equivalent in size and function.

EXAMPLE I Influence of the Origin of the Microsilica Slag compositions are formulated with the three different microsilices in Table 1 below.

TABLE 1

These microsilicates are incorporated into the following formulation (% by weight relative to the cement):

Portland cement class G: 100 silica (crushed quartz): 20 fluidizer D80 (Do ell): 1.8 Total water: 27 microsilica: 24

Formulation A with microsilica a Formulation B with microsilica b Formulation C with microsilica c

The rheological properties are shown in Figure 1.

The most favorable viscosity according to the criteria resulting from cementing operations on wells is obtained with microsilica a. Rheology criterion for a petroleum cement: For a flow law of the Os ald type (τ = K. γ ⁿ ) with K close to 0.5 and n close to 1, the equivalent density in circulation (ECD) remains below the value 0.5 accepted by the profession.

The equivalent density in circulation (ECD) is defined such that the pressure which undergoes the formation during the installation of the cement slag remains lower than the fracturing pressure of the tank.

The pumpability times, defined as the time necessary for the placement of the cement slag in the well with a minimum of 2 hours, are given in table 2 below gives for the 3 formulations, A, B, C.

TABLE 2

Formulation A is therefore the most efficient.

EXAMPLE II Choice of the fluidizer compared to the microsilica.

The following formulations, expressed in% by weight relative to the cement, are prepared:

- Portland cement class G: 100

- silica (as in Example 1): 20

- fluidizer: 1.8 - total water: 27

- microsilica a: 24 Formulation A: D80 polynaphthalene sulfonate thinner Formulation B: Styrene acrylate thinner

The viscosity is more favorable with the fluidizer of formulation A (fig. 2).

The behavior of formulation B is due to specific interactions between the thinner acrylate functions and the microsilica from the zirconium industry. It is therefore preferable to formulate with this type of microsilica fluidizers containing sulfonated or phosphated functions and to avoid the acrylate functions.

EXAMPLE III Optimization of the percentage of particles in relation to flow and pressure drop criteria for well cementing.

The main danger when placing the cement slag is the generation of pressures greater than the fracturing pressures of the rocks crossed during drilling. The pressures generated by the injection of fluids, in particular cement, through the completion of a well are due to friction. For this type of operation, an important factor is the control of the flow of the cement slag and therefore the knowledge of its rheological behavior. From a particular choice of operational parameters, the acceptable pressure and pressure losses are deduced, taking into account the rheology of the cement slag.

The choice of composition is made by optimizing the rheology from a certain amount of fixed water.

The following formulations, expressed in% relative to the cement, are prepared: - Portland cement class G: 100

- Silica (as in Example 1)

- Fluidifier (as in Example 1): 1.8

- Total water: 27 - Microsilica has:

Formulation A: Microsilica a at 24% and silica at 20%

Formulation Bl: Microsilica a at 30% and silica at 20%

Formulation B2: Microsilica a at 35% and silica at 20% Formulation Cl: Microsilica a at ^" 24% and silica at 40%

Formulation C2: Microsilica a at 24% and silica at 60%

These formulations provided the results shown in Figure 3.

Optimization of fine particles: (A) in comparison with (Bl) and (B2).

The more the quantity of fines increases, the more the particles can flow through an effect similar to a ball bearing and therefore the more fluid the slag is. A limit in viscosity improvement is reached if we compare the flow curves -B1 and B2. An optimal percentage of fines, between 20 and 35%, is thus determined.

Optimization of average particles: (A) in comparison with (Cl) and (C2).

Likewise, the relative percentage of average particles compared to fine particles is determined if we compare the flow curves Cl and C2 compared to that of A.

Formulations Cl and C2 contain more medium particles compared to fine particles (microsilica), and then have a rheology (curves Cl and C2 in FIG. 3) greater than formulations Bl-B2, A, all of which have an amount of average particles lower than that of fine particles. The cement slags having a rheology comparable to that of Cl or C2, are ill-suited, or even not suitable for the cementing of oil wells.

Indeed, this is confirmed by another test on formulations with the amounts of silica and microsilica collected in Table 3 below. The results of these tests (τ in (Pa)) are also given in Table 3.

TABLE 3

τ (Pa) represents the values and stresses measured for

-1 a given shear of 100 Formulations with stress values less than

130 Pa are obtained for microsilica / silica ratios at most equal to 1.

In the case of the relatively high rate of

35% microsilica, a test gives, for 35% of average particles, a stress value of the order of 130 Pa which represents a rheology which is sometimes acceptable, but generally limited.

For the formulation containing 60% of silica and between 20 to 35% of microsilica, the shear stresses are too great for the present application.

For an amount of fines of the order of 24%, an amount by weight of average particles of 20% gives good rheology for a well geometry classic.

In addition, formulation A which contains water in a water to cement ratio of 0.27 has a compressive strength 3.5 times greater than a conventional formulation of cement for wells which contains water in a ratio water on cement greater than 0.4.

EXAMPLE IV Comparison of the properties of a formulation of conventional cement slag with a formulation according to the present invention.

The main properties required for petroleum cement are listed below. A systematic comparison is made between the formulation of invention A and a conventional petroleum cement (B).

Formulation A expressed in% relative to the cement

- cement (as in Example 1): 100

- Silica (as in Example 1): 20 - D 80 thinner (as in Example 1): 1.8

- Total water: 27

- microsilica a: 24 '

- Retarder D 121 (Do εll): 0.8 Formulation B expressed in% relative to the cement - cement (as in example 1)): 100

- Silica S8 (Sifraco): 40

- Filler Microblock (Halliburton): 14.3

- Halad 361 A filtrate reducer (Halliburton): 8.5

- Dispersant: CFR3 (Halliburton): 0.25 - HR 15 retarder (Halliburton): 0.7

- Total water: 44%

Figure 4 shows a lower viscosity curve for formulation (A), which further limits the pressure drops in the well. The compressive strength, the time of pumpability, that is to say the time necessary for the establishment of the slag in the well and for the solidification of the slag, and the density optimized to control the pressure during the partial establishment in the case of hot wells and deep, are reported in Table 4 below. This table confirms the performance of the cement slag based on formulation A, in particular for the cementing of hot and deep wells.

TABLE 4

Claims

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14

1 / Cement slag for cementing a well, in particular an oil well, characterized in that it comprises:

- at least one hydraulic binder from the group consisting of Portland cements class G (API), Portland cements class H (API) and „_other hydraulic binders with a low aluminate content,

- a microsilica with a particle size in the range 0.1 to 50 micrometers, at a rate of 20 to 35% by weight relative to the hydraulic binder.

- an addition of medium, inorganic and / or organic particles, of grain size included in the range

0.5-200 micrometers at a rate of 20 to 35% by weight relative to the hydraulic binder, the amount of said addition of medium particles being less than or equal to the amount of microsilica, - a water-soluble superplasticizer and / or fluidizer in proportion included between 1% and 3% by weight relative to the hydraulic binder, and

- water in an amount at most equal to 30% of the weight of the hydraulic binder. 2 _ Dairy according to claim 1, whose hydraulic binder is a Portland cement class G.

3 / Dairy according to claim 1 or 2, whose hydraulic binder consists of particles whose sizes are distributed in the range 0.1-100 micrometers.

4 / Dairy according to claim 3, whose hydraulic binder consists of particles whose sizes are distributed in the range 10-50 micrometers. 5 / Dairy according to one of claims 1 to 4, the microsilica is a silica fume from the zirconium industry.

6 / Dairy according to one of the preceding claims in which the microsilica is present in an amount of 20-30% by weight relative to the hydraulic binder.

7 / Dairy according to one of the preceding claims in which the microsilica is present in an amount of 20 to 25% by weight relative to the hydraulic binder.

8 / Dairy according to one of the preceding claims in which the microsilica consists of agglomerate and particles whose average size is close to 3 micrometers. 9 / Dairy according to any one of the preceding claims, the addition of medium particles is an organic addition of plastic beads.

10 / Dairy according to claim 9 wherein the plastic is polystyrene.

11 / Dairy according to one of claims 1 to 8, the addition of medium particles is a mineral addition chosen from silica, clay, glass beads, metal salts, baryte, hematite and 1 ' ilmenite. 12 / Dairy according to one of claims 1 to 8, the addition of medium particles is a mineral addition of siliceous particles.

13 / -Dairy according to one of the preceding claims in which the addition of medium particles is present in an amount of 20 to 30% by weight relative to the hydraulic binder. 14 / Dairy according to one of claims 1 to 8, 12 and 13, the addition of medium particles is a mineral addition of silica sand whose particles have sizes distributed in the range 5-200 micrometers. 15 / Dairy according to one of claims 1 to 8 and 12 to

14 of which the addition of medium particles is an addition mineral of siliceous sand whose particles have an average size close to 50 micrometers.

16 / Dairy according to one of claims 1 to 8 and 12 to

14, the addition of medium particles of which is a mineral addition of ground quartz.

17 / Dairy according to one of the preceding claims, the water-soluble agent of which is composed of highly ionized polymer or copolymer derived from sulfonated functions and / or from phosphate, phosphonate, carboxylate. 18 / Dairy according to any one ^" of claims 1 to

16, the water-soluble agent of which is an agent from the group consisting of naphthalene sulfonate, lignosulfate, melanin and the like. 19 / Dairy according to one of the preceding claims, the water-soluble agent of which is a fluidizer containing sulfonated or phosphated functions. 20 / Dairy according to one of the preceding claims, the amount of water is in the range 20-30% of the weight of the hydraulic binder.